US8084160B2 - Method for purifying lithium sulfide - Google Patents
Method for purifying lithium sulfide Download PDFInfo
- Publication number
- US8084160B2 US8084160B2 US10/576,721 US57672104A US8084160B2 US 8084160 B2 US8084160 B2 US 8084160B2 US 57672104 A US57672104 A US 57672104A US 8084160 B2 US8084160 B2 US 8084160B2
- Authority
- US
- United States
- Prior art keywords
- lithium
- lithium sulfide
- organic solvent
- sulfide
- pyrrolidone
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related, expires
Links
- GLNWILHOFOBOFD-UHFFFAOYSA-N lithium sulfide Chemical compound [Li+].[Li+].[S-2] GLNWILHOFOBOFD-UHFFFAOYSA-N 0.000 title claims abstract description 94
- 238000000034 method Methods 0.000 title claims abstract description 47
- 239000003960 organic solvent Substances 0.000 claims abstract description 38
- WMFOQBRAJBCJND-UHFFFAOYSA-M Lithium hydroxide Chemical compound [Li+].[OH-] WMFOQBRAJBCJND-UHFFFAOYSA-M 0.000 claims abstract description 33
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229910000037 hydrogen sulfide Inorganic materials 0.000 claims abstract description 15
- SECXISVLQFMRJM-UHFFFAOYSA-N N-Methylpyrrolidone Chemical compound CN1CCCC1=O SECXISVLQFMRJM-UHFFFAOYSA-N 0.000 claims description 61
- 238000005406 washing Methods 0.000 claims description 27
- 239000007784 solid electrolyte Substances 0.000 claims description 22
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 claims description 20
- 229910052744 lithium Inorganic materials 0.000 claims description 20
- 239000007787 solid Substances 0.000 claims description 12
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 claims description 12
- 229910052815 sulfur oxide Inorganic materials 0.000 claims description 10
- YGLBXEHGQGOHPL-UHFFFAOYSA-M lithium;2-(methylamino)butanoate Chemical compound [Li+].CCC(NC)C([O-])=O YGLBXEHGQGOHPL-UHFFFAOYSA-M 0.000 claims description 9
- 238000010908 decantation Methods 0.000 claims description 8
- 238000009835 boiling Methods 0.000 claims description 7
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 6
- 239000011261 inert gas Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 3
- BSJWDQYZFBYNIM-UHFFFAOYSA-N 1,3,4,5-tetramethylpyrrolidin-2-one Chemical compound CC1C(C)N(C)C(=O)C1C BSJWDQYZFBYNIM-UHFFFAOYSA-N 0.000 claims description 2
- BCNBMSZKALBQEF-UHFFFAOYSA-N 1,3-dimethylpyrrolidin-2-one Chemical compound CC1CCN(C)C1=O BCNBMSZKALBQEF-UHFFFAOYSA-N 0.000 claims description 2
- NCNWTBAWLAFYDR-UHFFFAOYSA-N 1,6-dimethylpiperidin-2-one Chemical compound CC1CCCC(=O)N1C NCNWTBAWLAFYDR-UHFFFAOYSA-N 0.000 claims description 2
- SZMLDVKZMIXAJF-UHFFFAOYSA-N 1-(2-methylpropyl)azepan-2-one Chemical compound CC(C)CN1CCCCCC1=O SZMLDVKZMIXAJF-UHFFFAOYSA-N 0.000 claims description 2
- IVUYGANTXQVDDG-UHFFFAOYSA-N 1-(2-methylpropyl)pyrrolidin-2-one Chemical compound CC(C)CN1CCCC1=O IVUYGANTXQVDDG-UHFFFAOYSA-N 0.000 claims description 2
- ZFPGARUNNKGOBB-UHFFFAOYSA-N 1-Ethyl-2-pyrrolidinone Chemical compound CCN1CCCC1=O ZFPGARUNNKGOBB-UHFFFAOYSA-N 0.000 claims description 2
- VGZOTUWVGXUNRC-UHFFFAOYSA-N 1-butylazepan-2-one Chemical compound CCCCN1CCCCCC1=O VGZOTUWVGXUNRC-UHFFFAOYSA-N 0.000 claims description 2
- BNXZHVUCNYMNOS-UHFFFAOYSA-N 1-butylpyrrolidin-2-one Chemical compound CCCCN1CCCC1=O BNXZHVUCNYMNOS-UHFFFAOYSA-N 0.000 claims description 2
- MXEOFTCIEDUHCX-UHFFFAOYSA-N 1-cyclohexylazepan-2-one Chemical compound O=C1CCCCCN1C1CCCCC1 MXEOFTCIEDUHCX-UHFFFAOYSA-N 0.000 claims description 2
- IVVVGBHWWAJRAY-UHFFFAOYSA-N 1-ethyl-3-methylpyrrolidin-2-one Chemical compound CCN1CCC(C)C1=O IVVVGBHWWAJRAY-UHFFFAOYSA-N 0.000 claims description 2
- GWCFTYITFDWLAY-UHFFFAOYSA-N 1-ethylazepan-2-one Chemical compound CCN1CCCCCC1=O GWCFTYITFDWLAY-UHFFFAOYSA-N 0.000 claims description 2
- VUQMOERHEHTWPE-UHFFFAOYSA-N 1-ethylpiperidin-2-one Chemical compound CCN1CCCCC1=O VUQMOERHEHTWPE-UHFFFAOYSA-N 0.000 claims description 2
- GGYVTHJIUNGKFZ-UHFFFAOYSA-N 1-methylpiperidin-2-one Chemical compound CN1CCCCC1=O GGYVTHJIUNGKFZ-UHFFFAOYSA-N 0.000 claims description 2
- BWIRRVWVFWVVSG-UHFFFAOYSA-N 1-propan-2-ylazepan-2-one Chemical compound CC(C)N1CCCCCC1=O BWIRRVWVFWVVSG-UHFFFAOYSA-N 0.000 claims description 2
- GVDQKJQFVPXADH-UHFFFAOYSA-N 1-propan-2-ylpiperidin-2-one Chemical compound CC(C)N1CCCCC1=O GVDQKJQFVPXADH-UHFFFAOYSA-N 0.000 claims description 2
- GHELJWBGTIKZQW-UHFFFAOYSA-N 1-propan-2-ylpyrrolidin-2-one Chemical compound CC(C)N1CCCC1=O GHELJWBGTIKZQW-UHFFFAOYSA-N 0.000 claims description 2
- BWISIXSYQURMMY-UHFFFAOYSA-N 1-propylazepan-2-one Chemical compound CCCN1CCCCCC1=O BWISIXSYQURMMY-UHFFFAOYSA-N 0.000 claims description 2
- DCALJVULAGICIX-UHFFFAOYSA-N 1-propylpyrrolidin-2-one Chemical compound CCCN1CCCC1=O DCALJVULAGICIX-UHFFFAOYSA-N 0.000 claims description 2
- DRYYJQYUHPRVBN-UHFFFAOYSA-N 3-ethyl-1-methylpiperidin-2-one Chemical compound CCC1CCCN(C)C1=O DRYYJQYUHPRVBN-UHFFFAOYSA-N 0.000 claims description 2
- FXHOOIRPVKKKFG-UHFFFAOYSA-N N,N-Dimethylacetamide Chemical compound CN(C)C(C)=O FXHOOIRPVKKKFG-UHFFFAOYSA-N 0.000 claims description 2
- SUAKHGWARZSWIH-UHFFFAOYSA-N N,N‐diethylformamide Chemical compound CCN(CC)C=O SUAKHGWARZSWIH-UHFFFAOYSA-N 0.000 claims description 2
- ZWXPDGCFMMFNRW-UHFFFAOYSA-N N-methylcaprolactam Chemical compound CN1CCCCCC1=O ZWXPDGCFMMFNRW-UHFFFAOYSA-N 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims description 2
- IMNDHOCGZLYMRO-UHFFFAOYSA-N n,n-dimethylbenzamide Chemical compound CN(C)C(=O)C1=CC=CC=C1 IMNDHOCGZLYMRO-UHFFFAOYSA-N 0.000 claims description 2
- IFTIBNDWGNYRLS-UHFFFAOYSA-N n,n-dipropylacetamide Chemical compound CCCN(C(C)=O)CCC IFTIBNDWGNYRLS-UHFFFAOYSA-N 0.000 claims description 2
- PZYDAVFRVJXFHS-UHFFFAOYSA-N n-cyclohexyl-2-pyrrolidone Chemical compound O=C1CCCN1C1CCCCC1 PZYDAVFRVJXFHS-UHFFFAOYSA-N 0.000 claims description 2
- 239000006185 dispersion Substances 0.000 claims 3
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 claims 2
- 239000012535 impurity Substances 0.000 abstract description 20
- 238000000746 purification Methods 0.000 abstract description 3
- 230000000052 comparative effect Effects 0.000 description 19
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 238000004519 manufacturing process Methods 0.000 description 11
- 239000000243 solution Substances 0.000 description 9
- 239000002002 slurry Substances 0.000 description 8
- 239000002994 raw material Substances 0.000 description 7
- -1 and then Chemical compound 0.000 description 6
- BBLSYMNDKUHQAG-UHFFFAOYSA-L dilithium;sulfite Chemical compound [Li+].[Li+].[O-]S([O-])=O BBLSYMNDKUHQAG-UHFFFAOYSA-L 0.000 description 6
- 230000007774 longterm Effects 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- INHCSSUBVCNVSK-UHFFFAOYSA-L lithium sulfate Inorganic materials [Li+].[Li+].[O-]S([O-])(=O)=O INHCSSUBVCNVSK-UHFFFAOYSA-L 0.000 description 5
- 239000003495 polar organic solvent Substances 0.000 description 4
- 125000003368 amide group Chemical group 0.000 description 3
- GMKDNCQTOAHUQG-UHFFFAOYSA-L dilithium;dioxido-oxo-sulfanylidene-$l^{6}-sulfane Chemical compound [Li+].[Li+].[O-]S([O-])(=O)=S GMKDNCQTOAHUQG-UHFFFAOYSA-L 0.000 description 3
- 150000002898 organic sulfur compounds Chemical class 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- RBTVSNLYYIMMKS-UHFFFAOYSA-N tert-butyl 3-aminoazetidine-1-carboxylate;hydrochloride Chemical compound Cl.CC(C)(C)OC(=O)N1CC(N)C1 RBTVSNLYYIMMKS-UHFFFAOYSA-N 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- 230000006866 deterioration Effects 0.000 description 2
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 150000002894 organic compounds Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 150000003672 ureas Chemical class 0.000 description 2
- XTHFKEDIFFGKHM-UHFFFAOYSA-N Dimethoxyethane Chemical compound COCCOC XTHFKEDIFFGKHM-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- IKJFYINYNJYDTA-UHFFFAOYSA-N dibenzothiophene sulfone Chemical compound C1=CC=C2S(=O)(=O)C3=CC=CC=C3C2=C1 IKJFYINYNJYDTA-UHFFFAOYSA-N 0.000 description 1
- CCAFPWNGIUBUSD-UHFFFAOYSA-N diethyl sulfoxide Chemical compound CCS(=O)CC CCAFPWNGIUBUSD-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000002305 electric material Substances 0.000 description 1
- 239000012776 electronic material Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000004255 ion exchange chromatography Methods 0.000 description 1
- HXQGSILMFTUKHI-UHFFFAOYSA-M lithium;sulfanide Chemical compound S[Li] HXQGSILMFTUKHI-UHFFFAOYSA-M 0.000 description 1
- 239000002798 polar solvent Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
Classifications
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/056—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes
- H01M10/0561—Accumulators with non-aqueous electrolyte characterised by the materials used as electrolytes, e.g. mixed inorganic/organic electrolytes the electrolyte being constituted of inorganic materials only
- H01M10/0562—Solid materials
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01D—COMPOUNDS OF ALKALI METALS, i.e. LITHIUM, SODIUM, POTASSIUM, RUBIDIUM, CAESIUM, OR FRANCIUM
- C01D15/00—Lithium compounds
- C01D15/06—Sulfates; Sulfites
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/22—Alkali metal sulfides or polysulfides
- C01B17/36—Purification
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M10/00—Secondary cells; Manufacture thereof
- H01M10/05—Accumulators with non-aqueous electrolyte
- H01M10/052—Li-accumulators
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/80—Compositional purity
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M2300/00—Electrolytes
- H01M2300/0017—Non-aqueous electrolytes
- H01M2300/0065—Solid electrolytes
- H01M2300/0068—Solid electrolytes inorganic
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/10—Energy storage using batteries
Definitions
- the invention relates to a method of purifying lithium sulfide by which impurities such as sulfur oxides and lithium N-methylaminobutyrate (hereinafter referred to as LMAB) can efficiently be removed from lithium sulfide used for electronic and electric materials. Further, the invention relates to a solid electrolyte for a lithium rechargeable battery and a solid battery using the same.
- impurities such as sulfur oxides and lithium N-methylaminobutyrate (hereinafter referred to as LMAB) can efficiently be removed from lithium sulfide used for electronic and electric materials.
- LMAB lithium N-methylaminobutyrate
- the rechargeable battery is a battery capable of being charged and discharged. During use, the rechargeable battery is subjected to repeated charge and discharge over a long period of time. Its components therefore have to have long-term stability and durability.
- lithium sulfide is produced in an aprotic organic solvent such as N-methyl-2-pyrrolidone (hereinafter referred to as NMP), and it is an economical and simple method because the production steps thereof can be conducted continuously.
- NMP N-methyl-2-pyrrolidone
- LMAB which is an impurity derived from NMP, comes to be mixed in the resultant lithium sulfide.
- JP-A-H09-283156 discloses a method of producing lithium sulfide wherein lithium hydroxide and a gaseous sulfur source are reacted at a temperature of at lowest 130° C. to at highest 445° C.
- Sulfur oxides (such as lithium sulfite, lithium sulfate, and lithium thiosulfate) which are formed in the production process of lithium sulfide come to be mixed in the lithium sulfide produced by this method.
- the lithium sulfide produced by the above-mentioned methods is used as a raw material of a solid electrolyte for a lithium rechargeable battery or the like, the solid electrolyte deteriorates due to the repetition of charge and discharge, and the desired battery performance cannot be realized.
- One object of the invention is to solve the above-mentioned problems by providing a method of purifying lithium sulfide wherein impurities contained in lithium sulfide constituting a raw material for a solid electrolyte of a lithium rechargeable battery are minimized.
- Another object of the invention is to provide a solid electrolyte for a lithium rechargeable battery using lithium sulfide in which the impurities are minimal, and a solid battery using the same.
- the inventors carried out committed studies to achieve these objects, and found that the impurities can be efficiently removed from the lithium sulfide produced by the method disclosed in the above-mentioned JP-A-H07-330312 by washing it with an organic solvent having a boiling point of 100° C. or higher, such as NMP, at a temperature of 100° C. or higher.
- an organic solvent having a boiling point of 100° C. or higher, such as NMP at a temperature of 100° C. or higher.
- the invention was accomplished on the basis of this finding.
- the invention provides a method of purifying lithium sulfide wherein lithium sulfide obtained by reacting lithium hydroxide with hydrogen sulfide in an aprotic organic solvent is washed with an organic solvent at a temperature of 100° C. or higher.
- the invention provides a solid electrolyte for a lithium rechargeable battery using the lithium sulfide purified by the above-mentioned method of the first aspect.
- the invention provides a solid battery using the solid electrolyte for a lithium rechargeable battery of the above-mentioned second aspect.
- lithium sulfide in which the contents of sulfur oxides are reduced to 0.15% by weight or less and the content of LMAB is reduced to 0.1% by weight can economically be obtained.
- the method of purifying lithium sulfide of the first aspect of the invention (hereinafter referred to as the method of the invention) is characterized in that lithium sulfide produced by reacting lithium hydroxide with hydrogen sulfide in an aprotic organic solvent is washed with an organic solvent at a temperature of 100° C. or higher.
- the lithium sulfide to be purified by the method of the invention is one produced by the method of producing lithium sulfide disclosed in JP-A-H07-330312.
- lithium hydroxide is reacted with hydrogen sulfide at a temperature of 0 to 150° C. while injecting hydrogen sulfide into an aprotic organic solvent, to form lithium hydrosulfide, and then, hydrogen sulfide is removed from the reaction solution at a temperature of 150 to 200° C. without injection of hydrogen sulfide to obtain lithium sulfide, or lithium hydroxide and hydrogen sulfide are reacted in an aprotic organic solvent at a temperature of 150 to 200° C. to directly produce lithium sulfide.
- an aprotic polar organic solvent such as amido compounds, lactam compounds, urea compounds, organic sulfur compounds, and cyclic organic phosphorous compounds
- an aprotic polar organic solvent such as amido compounds, lactam compounds, urea compounds, organic sulfur compounds, and cyclic organic phosphorous compounds
- N-methyl-2-pyrrolidone N-alkylcaprolactam and N-alkylpyrrolidone
- particularly preferred is N-methyl-2-pyrrolidone
- the lithium hydroxide used as raw material for production of lithium sulfide is not particularly limited, and a commercially available product can be used so long as it is of high purity.
- the other raw material, hydrogen sulfide, is also not particularly limited. Further, reaction conditions for the production of lithium sulfide, the relative amounts of the raw materials used, and the like are determined as set out in JP-A-H07-330312.
- the method of the invention is characterized by using the lithium sulfide produced by the above-mentioned method disclosed in JP-A-H07-330312, and washing it with an organic solvent at a temperature of 100° C. or higher.
- the organic solvent is used at a temperature of 100° C. or higher because LMAB, which is an impurity, formed in the case where NMP is used as the aprotic organic solvent for the production of lithium sulfide, dissolves in the organic solvent at a temperature of 100° C. Namely, LMAB dissolves in the organic solvent for washing to remove it from lithium sulfide.
- the temperature of the organic solvent used is not particularly limited so long as it is 100° C. or higher, and may arbitrarily be selected. However, the temperature of the organic solvent used is lower than its boiling point. For instance, when using NMP, the temperature is at highest 203° C., the boiling point at normal pressures, and at highest 250° C. under pressure in the case where a well-closed vessel or the like is used.
- the organic solvent used for washing in the method of the invention is preferably an aprotic polar solvent. Further, it is more preferred that the aprotic organic solvent used for production of lithium sulfide be identical to the aprotic polar organic solvent used for washing.
- aprotic polar organic solvents used for washing include aprotic polar organic compounds such as amido compounds, lactam compounds, urea compounds, organic sulfur compounds, and cyclic organic phosphorous compounds. They may be used preferably either individually or in a mixture.
- aprotic polar organic solvents include N,N-dimethylformamide, N,N-diethylformamide, N,N-dimethylacetamide, N,N-dipropylacetamide, and N,N-dimethyl benzoic acid amide.
- lactam compounds include caprolactam; N-alkylcaprolactams such as N-methylcaprolactam, N-ethylcaprolactam, N-isopropylcaprolactam, N-isobutylcaprolactam, N-n-propylcaprolactam, N-n-butylcaprolactam, and N-cyclohexylcaprolactam; N-methyl-2-pyrrolidone (NMP), N-ethyl-2-pyrrolidone, N-isopropyl-2-pyrrolidone, N-isobutyl-2-pyrrolidone, N-n-propyl-2-pyrrolidone, N-n-butyl-2-pyrrolidone, N-cyclohexyl-2-pyrrolidone, N-methyl-3-methyl-2-pyrrolidone, N-ethyl-3-methyl-2-pyrrolidone, N-methyl-3,4,5-trimethyl-2-pyrrolidone
- the above-mentioned organic sulfur compounds include dimethyl sulfoxide, diethyl sulfoxide, diphenylene sulfone, 1-methyl-1-oxosulfolane, and 1-phenyl-1-oxosulfolane.
- aprotic organic compounds may be used, as the above-mentioned aprotic organic solvent, individually or in a mixture of two or more, alternatively used in a mixture with another solvent component which does not hinder achievement of the object of the invention.
- N-alkylcaprolactam and N-alkylpyrrolidone are preferred, and N-methyl-2-pyrrolidone (NMP) is particularly preferred.
- the amount of the organic solvent used for washing is not particularly limited, and the number of times for washing is also not particularly limited but is preferably twice or more.
- the washing is preferably carried out under an inert gas such as nitrogen or argon.
- Lithium sulfide is produced by the method disclosed in the above-mentioned JP-A-H07-330312 using NMP as the aprotic organic solvent.
- NMP-lithium sulfide slurry The NMP in the resultant reaction solution slurry (NMP-lithium sulfide slurry) is removed by decantation or filtration at a temperature of 100° C. or higher.
- Fresh NMP is added to the resultant crude lithium sulfide to wash the lithium sulfide at a temperature of 100° C. or higher, followed by decantation or filtration at a temperature of 100° C. or higher under an inert gas such as nitrogen. This washing operation is carried out once or more.
- the lithium sulfide after washing is dried at a temperature of at lowest the boiling point of the NMP used for washing under a stream of an inert gas such as nitrogen and at normal pressure or under reduced pressure for 5 minutes or more (preferably approximately 2 to 3 hours or more), to obtain purified lithium sulfide.
- highly purified lithium sulfide in which the total content of sulfur oxides is 0.15% by weight or less, preferably 0.1% by weight or less, and the content of lithium N-methylaminobutyrate (LMAB) is 0.1% by weight or less.
- LMAB lithium N-methylaminobutyrate
- the number of washings is considered to be about 10 or less. Repetition of the washing about 10 times enables reduction of the total sulfur oxides content to approximately 0.001% by weight and the lithium N-methylaminobutyrate (LMAB) content to approximately 0.0005% by weight.
- the solid electrolyte synthesized by using the lithium sulfide purified by the method of the invention has electrical properties suitable for a solid electrolyte for a lithium rechargeable battery, such as an ionic conductance of 1.0 ⁇ 10 ⁇ 3 s/cm or higher, preferably 1.1 ⁇ 10 ⁇ 3 s/cm or higher.
- the lithium sulfide purified by the method of the invention is reduced in impurities that adversely affect the long-term stability of a battery. Further, although it is not known exactly why, the manner in which the impurities are contained in the lithium sulfide after purification gives rise to ionic conductance suitable for the solid electrolyte of a lithium rechargeable battery, and the desired battery performance can be maintained for a long period of time, even when charge and discharge are repeated.
- the solid battery excellent in long-term stability can be obtained by using the solid electrolyte for a lithium rechargeable battery having the good properties mentioned above.
- Lithium sulfide was produced in accordance with the first aspect (two-step method) disclosed in JP-A-H07-330312. Specifically, 3326.4 gram (33.6 moles) of N-methyl-2-pyrrolidone (NMP) and 287.4 gram (12 moles) of lithium hydroxide were charged into a 10 liter autoclave equipped with a stirring paddle and heated to 130° C. under stirring at 300 rpm. The heating was followed by injection of hydrogen sulfide into the reaction solution at a feed rate of 3 liter/minute for 2 hours. Subsequently, the temperature of the reaction solution was increased under a nitrogen stream (200 cc/minute) to remove a part of hydrogen sulfide which started generating from the reaction product.
- NMP N-methyl-2-pyrrolidone
- 287.4 gram (12 moles) of lithium hydroxide were charged into a 10 liter autoclave equipped with a stirring paddle and heated to 130° C. under stirring at 300 rpm.
- NMP was removed by decantation from 500 mL of the reaction solution slurry (NMP-lithium sulfide slurry) obtained in the above-mentioned step (1), and then, 100 mL of dehydrated NMP was added thereto and stirred at a temperature of 105° C. for about one hour. NMP was removed by decantation while maintaining the temperature of the slurry. One hundred mL of NMP was again added thereto and stirred at a temperature of 105° C. for about one hour. NMP was removed by decantation while maintaining the temperature of the slurry. This operation was repeated four times in total. After completion of the decantation, the lithium sulfide was dried at a temperature of 230° C. (at the NMP boiling point temperature or higher) under a nitrogen stream at normal pressure for three hours. The contents of the impurities contained in the resultant lithium sulfide were determined. The results are shown in Table 1 below.
- lithium sulfite Li 2 SO 3
- lithium sulfate Li 2 SO 4
- lithium thiosulfate Li 2 S 2 O 3
- lithium N-methylaminobutyrate LMAB
- Lithium sulfide was obtained in the same manner as in Example 1 except that the drying conditions were changed from at a temperature of 230° C. under nitrogen stream at normal pressures to at a temperature of 230° C. under reduced pressure. The contents of the impurities contained in the resultant lithium sulfide were determined, and the results are shown in Table 1 below.
- Lithium sulfide was obtained in the same manner as in Example 2 except that washing with NMP was repeated ten times. The contents of the impurities contained in the resultant lithium sulfide were determined, and the results are shown in Table 1 below.
- NMP was removed by decantation from 500 mL of the reaction solution slurry (NMP-lithium sulfide slurry) produced in Example 1 and the impurity contents of the so-obtained crude lithium sulfide (i.e., lithium sulfide not subjected to NMP washing) were determined.
- the results are shown in Table 1 below.
- Lithium sulfide was obtained in the same manner as in Example 1 except that the washing temperature was changed from 105° C. to normal temperature. The contents of the impurities contained in the resultant lithium sulfide were determined, and the results are shown in Table 1 below.
- Lithium sulfide was obtained in the same manner as in Example 1 except that the washing solvent was changed to dimethoxyethane (boiling point: 82 to 83° C.), and the washing temperature was changed to 70° C.
- the contents of the impurities contained in the resultant lithium sulfide were determined, and the results are shown in Table 1 below.
- Comparative Example 4 lithium sulfite; manufactured by Aldrich Chemical Company, Inc.
- Comparative Example 5 lithium sulfite; manufactured by Furuuchi Chemical Corporation
- Comparative Example 6 lithium sulfite; manufactured by Kishida Chemical Co., Ltd.
- the lithium sulfide of Comparative Example 2 which was obtained by washing at a temperature lower than 100° C., was lowered to the same level of lithium sulfite and lithium sulfate contents as the purified lithium sulfide obtained in Examples 1 and 2 but was not reduced in lithium thiosulfate and lithium N-methylaminobutyrate (LMAB) contents.
- LMAB lithium N-methylaminobutyrate
- Example 1 and Comparative example 2 demonstrated that the desired washing effect cannot be obtained by washing at a temperature lower than 100° C., even when using the same solvent.
- the invention further provides a solid electrolyte for a lithium rechargeable battery that is excellent in long-term stability and a solid battery using the same, which is excellent battery performance.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Manufacturing & Machinery (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Physics & Mathematics (AREA)
- Condensed Matter Physics & Semiconductors (AREA)
- General Physics & Mathematics (AREA)
- Materials Engineering (AREA)
- Secondary Cells (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2003363403 | 2003-10-23 | ||
JP2003-363403 | 2003-10-23 | ||
PCT/JP2004/015231 WO2005040039A1 (ja) | 2003-10-23 | 2004-10-15 | 硫化リチウムの精製方法 |
Publications (2)
Publication Number | Publication Date |
---|---|
US20070196739A1 US20070196739A1 (en) | 2007-08-23 |
US8084160B2 true US8084160B2 (en) | 2011-12-27 |
Family
ID=34510038
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/576,721 Expired - Fee Related US8084160B2 (en) | 2003-10-23 | 2004-10-15 | Method for purifying lithium sulfide |
Country Status (8)
Country | Link |
---|---|
US (1) | US8084160B2 (de) |
EP (1) | EP1681263B1 (de) |
JP (1) | JP4896520B2 (de) |
KR (1) | KR101109821B1 (de) |
CN (2) | CN1871177B (de) |
AT (1) | ATE513788T1 (de) |
TW (1) | TW200530121A (de) |
WO (1) | WO2005040039A1 (de) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9017582B2 (en) | 2011-05-27 | 2015-04-28 | Chemetall Gmbh | Process for preparing lithium sulfide |
US10865108B2 (en) | 2016-12-14 | 2020-12-15 | Idemitsu Kosan Co., Ltd | Complex comprising sulfur, a method for manufacturing the same, and a method for manufacturing a solid electrolyte |
Families Citing this family (46)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101326673B (zh) | 2005-12-09 | 2010-11-17 | 出光兴产株式会社 | 锂离子传导性硫化物类固体电解质及使用其的全固体锂电池 |
KR101442306B1 (ko) | 2007-10-11 | 2014-09-22 | 이데미쓰 고산 가부시키가이샤 | 리튬 이온 전도성 고체 전해질의 제조 방법 |
MX2010014201A (es) | 2008-07-18 | 2011-04-07 | Rincon Lithium Ltd | Proceso para la recuperacion de litio a partir de salmuera. |
JP2010126422A (ja) * | 2008-11-28 | 2010-06-10 | Panasonic Corp | リチウム含有複合酸化物の製造方法および非水系二次電池 |
JP5448038B2 (ja) | 2009-02-27 | 2014-03-19 | 公立大学法人大阪府立大学 | 硫化物固体電解質材料 |
JP5287739B2 (ja) | 2009-05-01 | 2013-09-11 | トヨタ自動車株式会社 | 固体電解質材料 |
JP5590836B2 (ja) | 2009-09-09 | 2014-09-17 | 公立大学法人大阪府立大学 | 硫化物固体電解質 |
JP5168269B2 (ja) | 2009-11-25 | 2013-03-21 | トヨタ自動車株式会社 | Liイオン伝導性材料およびリチウム電池 |
JP5629198B2 (ja) * | 2009-12-04 | 2014-11-19 | 出光興産株式会社 | アルカリ金属硫化物及びその製造方法 |
JP5141675B2 (ja) | 2009-12-16 | 2013-02-13 | トヨタ自動車株式会社 | 硫化物固体電解質材料の製造方法、硫化物固体電解質材料およびリチウム電池 |
AU2010358633B2 (en) | 2010-08-05 | 2014-08-07 | Toyota Jidosha Kabushiki Kaisha | Sulfide solid electrolyte glass, lithium solid-state battery, and method for producing sulfide solid electrolyte glass |
JP5729940B2 (ja) * | 2010-08-13 | 2015-06-03 | 出光興産株式会社 | 固体電解質ガラス及びその製造方法 |
JP5521899B2 (ja) | 2010-08-26 | 2014-06-18 | トヨタ自動車株式会社 | 硫化物固体電解質材料およびリチウム固体電池 |
JP5349427B2 (ja) | 2010-08-26 | 2013-11-20 | トヨタ自動車株式会社 | 硫化物固体電解質材料、正極体およびリチウム固体電池 |
WO2012102037A1 (ja) * | 2011-01-27 | 2012-08-02 | 出光興産株式会社 | アルカリ金属硫化物と導電剤の複合材料 |
JP5708467B2 (ja) | 2011-03-18 | 2015-04-30 | トヨタ自動車株式会社 | スラリー、固体電解質層の製造方法、電極活物質層の製造方法、および全固体電池の製造方法 |
JP5708233B2 (ja) | 2011-05-18 | 2015-04-30 | トヨタ自動車株式会社 | 硫化物固体電解質材料の製造方法および硫化物固体電解質材料 |
DE102012209757A1 (de) * | 2011-06-14 | 2012-12-20 | Chemetall Gmbh | Verfahren zur Herstellung eines kohlenstoffbeschichteten Lithiumsulfids und dessen Verwendung |
JP5443445B2 (ja) | 2011-07-06 | 2014-03-19 | トヨタ自動車株式会社 | 硫化物固体電解質材料、リチウム固体電池、および、硫化物固体電解質材料の製造方法 |
JP5445527B2 (ja) | 2011-07-13 | 2014-03-19 | トヨタ自動車株式会社 | 硫化物固体電解質材料の製造方法 |
EP2759525B1 (de) | 2011-09-22 | 2017-07-26 | Idemitsu Kosan Co., Ltd | Glasteilchen |
JP6234665B2 (ja) | 2011-11-07 | 2017-11-22 | 出光興産株式会社 | 固体電解質 |
JP6203474B2 (ja) | 2011-11-24 | 2017-09-27 | 出光興産株式会社 | 電極材料、電極及びそれを用いたリチウムイオン電池 |
JP6243103B2 (ja) | 2012-06-29 | 2017-12-06 | 出光興産株式会社 | 正極合材 |
US9673482B2 (en) | 2012-11-06 | 2017-06-06 | Idemitsu Kosan Co., Ltd. | Solid electrolyte |
FR2997941B1 (fr) * | 2012-11-15 | 2023-03-03 | Arkema France | Procede de preparation de sulfure de metal alcalin |
JP5757284B2 (ja) | 2012-12-27 | 2015-07-29 | トヨタ自動車株式会社 | 硫化物固体電解質材料、リチウム固体電池、および、硫化物固体電解質材料の製造方法 |
JP6259617B2 (ja) | 2013-04-24 | 2018-01-10 | 出光興産株式会社 | 固体電解質の製造方法 |
WO2014192309A1 (ja) | 2013-05-31 | 2014-12-04 | 出光興産株式会社 | 固体電解質の製造方法 |
JP5673760B1 (ja) | 2013-09-13 | 2015-02-18 | トヨタ自動車株式会社 | 硫化物固体電解質の製造方法 |
CN103523806B (zh) * | 2013-10-22 | 2014-11-12 | 瓮福(集团)有限责任公司 | 一种高纯度无水硫酸锂的制备方法 |
WO2016067631A1 (ja) | 2014-10-31 | 2016-05-06 | 出光興産株式会社 | 硫化物ガラス及び結晶性固体電解質の製造方法、結晶性固体電解質、硫化物ガラス及び固体電池 |
JP6697398B2 (ja) | 2014-12-16 | 2020-05-20 | 出光興産株式会社 | 硫化リチウム製造用装置及び硫化リチウムの製造方法 |
CN104609376A (zh) * | 2015-01-30 | 2015-05-13 | 浙江工业大学 | 一种硫化锂粉体的制备方法 |
KR101684130B1 (ko) | 2015-06-16 | 2016-12-07 | 현대자동차주식회사 | 리튬 이온 전도성 황화물의 제조방법, 이에 의하여 제조된 리튬 이온 전도성 황화물, 및 이를 포함하는 고체전해질, 전고체 배터리 |
CN105016310A (zh) * | 2015-07-30 | 2015-11-04 | 广东先导稀材股份有限公司 | 一种高纯硫化锂的制备方法及装置 |
KR101930992B1 (ko) * | 2016-02-15 | 2018-12-19 | 한양대학교 산학협력단 | 황화물계 고체 전해질의 제조방법, 이로부터 제조된 황화물계 고체 전해질 및 이를 포함하는 전고체 리튬 이차전지 |
KR101886036B1 (ko) | 2016-08-22 | 2018-08-07 | 한국과학기술연구원 | 대기 안정성이 우수한 황화물계 고체전해질의 제조방법 |
CN110790239B (zh) * | 2019-08-26 | 2022-01-28 | 浙江工业大学 | 一种硫化锂粉体的机械球磨合成方法 |
CN112678781B (zh) * | 2019-10-18 | 2022-04-15 | 天齐锂业(江苏)有限公司 | 硫化锂的制备方法 |
JP2023513622A (ja) | 2020-02-17 | 2023-03-31 | ソリッド パワー,インコーポレイティド | 水反応性の硫化物材料の製造方法 |
CN112624060B (zh) * | 2020-12-31 | 2022-09-20 | 江西赣锋锂业股份有限公司 | 一种利用工业级丁基锂制备高纯硫化锂的方法 |
KR20230129118A (ko) * | 2022-02-28 | 2023-09-06 | 주식회사 레이크테크놀로지 | 황화리튬 제조 장치 |
WO2023191417A1 (ko) * | 2022-03-31 | 2023-10-05 | 주식회사 솔리비스 | 고순도의 알칼리 금속황화물의 제조방법 |
KR102666522B1 (ko) * | 2022-11-10 | 2024-05-16 | 전북대학교산학협력단 | 황화 리튬의 제조방법 |
WO2024151153A1 (ko) * | 2023-01-12 | 2024-07-18 | 주식회사 이수스페셜티케미컬 | 황화 리튬의 제조 방법 |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07330312A (ja) | 1994-06-03 | 1995-12-19 | Idemitsu Petrochem Co Ltd | 硫化リチウムの製造方法 |
JPH09110404A (ja) | 1995-10-13 | 1997-04-28 | Furukawa Co Ltd | 硫化リチウムの製造方法 |
JPH09278423A (ja) | 1996-04-16 | 1997-10-28 | Furukawa Co Ltd | 硫化リチウムの製造方法 |
JPH09283156A (ja) | 1996-04-16 | 1997-10-31 | Matsushita Electric Ind Co Ltd | リチウムイオン伝導性固体電解質およびその製造方法 |
JPH09301706A (ja) | 1996-05-10 | 1997-11-25 | Matsushita Electric Ind Co Ltd | 固体電解質およびそれを用いた全固体リチウム電池 |
JPH10130005A (ja) | 1996-10-28 | 1998-05-19 | Idemitsu Petrochem Co Ltd | 硫化リチウムの製造方法及びポリアリーレンスルフィドの製造方法 |
US6022640A (en) * | 1996-09-13 | 2000-02-08 | Matsushita Electric Industrial Co., Ltd. | Solid state rechargeable lithium battery, stacking battery, and charging method of the same |
JP2000273175A (ja) | 1999-03-19 | 2000-10-03 | Idemitsu Petrochem Co Ltd | ポリアリーレンスルフィド系樹脂の精製方法 |
CN1333575A (zh) | 2000-07-19 | 2002-01-30 | 住友电气工业株式会社 | 制备锂二次电池负极的方法 |
US6455022B1 (en) * | 1991-06-10 | 2002-09-24 | Elf Atochem S.A. | Purification of aqueous alkali metal chloride solutions by removal of ammonium/iodine values therefrom |
US6503473B1 (en) * | 1999-03-08 | 2003-01-07 | Idemitsu Petrochemical Co., Ltd. | Process for separating solid compound other than lithium hydroxide |
JP2003068361A (ja) | 2001-08-23 | 2003-03-07 | Japan Storage Battery Co Ltd | 全固体リチウム二次電池 |
-
2004
- 2004-10-15 WO PCT/JP2004/015231 patent/WO2005040039A1/ja active Application Filing
- 2004-10-15 US US10/576,721 patent/US8084160B2/en not_active Expired - Fee Related
- 2004-10-15 EP EP04792448A patent/EP1681263B1/de not_active Not-in-force
- 2004-10-15 CN CN2004800309857A patent/CN1871177B/zh not_active Expired - Fee Related
- 2004-10-15 JP JP2005514938A patent/JP4896520B2/ja not_active Expired - Fee Related
- 2004-10-15 AT AT04792448T patent/ATE513788T1/de not_active IP Right Cessation
- 2004-10-15 CN CN2010100021743A patent/CN101980398A/zh active Pending
- 2004-10-15 KR KR1020067007700A patent/KR101109821B1/ko not_active IP Right Cessation
- 2004-10-22 TW TW093132259A patent/TW200530121A/zh not_active IP Right Cessation
Patent Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6455022B1 (en) * | 1991-06-10 | 2002-09-24 | Elf Atochem S.A. | Purification of aqueous alkali metal chloride solutions by removal of ammonium/iodine values therefrom |
JPH07330312A (ja) | 1994-06-03 | 1995-12-19 | Idemitsu Petrochem Co Ltd | 硫化リチウムの製造方法 |
JPH09110404A (ja) | 1995-10-13 | 1997-04-28 | Furukawa Co Ltd | 硫化リチウムの製造方法 |
JPH09283156A (ja) | 1996-04-16 | 1997-10-31 | Matsushita Electric Ind Co Ltd | リチウムイオン伝導性固体電解質およびその製造方法 |
JPH09278423A (ja) | 1996-04-16 | 1997-10-28 | Furukawa Co Ltd | 硫化リチウムの製造方法 |
JPH09301706A (ja) | 1996-05-10 | 1997-11-25 | Matsushita Electric Ind Co Ltd | 固体電解質およびそれを用いた全固体リチウム電池 |
US6022640A (en) * | 1996-09-13 | 2000-02-08 | Matsushita Electric Industrial Co., Ltd. | Solid state rechargeable lithium battery, stacking battery, and charging method of the same |
JPH10130005A (ja) | 1996-10-28 | 1998-05-19 | Idemitsu Petrochem Co Ltd | 硫化リチウムの製造方法及びポリアリーレンスルフィドの製造方法 |
US6503473B1 (en) * | 1999-03-08 | 2003-01-07 | Idemitsu Petrochemical Co., Ltd. | Process for separating solid compound other than lithium hydroxide |
JP2000273175A (ja) | 1999-03-19 | 2000-10-03 | Idemitsu Petrochem Co Ltd | ポリアリーレンスルフィド系樹脂の精製方法 |
CN1333575A (zh) | 2000-07-19 | 2002-01-30 | 住友电气工业株式会社 | 制备锂二次电池负极的方法 |
US20040109940A1 (en) * | 2000-07-19 | 2004-06-10 | Sumitomo Electric Industries, Ltd. | Method of producing negative electrode for lithium secondary cell |
JP2003068361A (ja) | 2001-08-23 | 2003-03-07 | Japan Storage Battery Co Ltd | 全固体リチウム二次電池 |
Non-Patent Citations (4)
Title |
---|
Database WPI Week 199727 Derwent Publications Ltd., London, GB; AN 1997-294617 XP002480255 & JP 09 110404 A (Furukawa Kikai Kinzoku KK) Apr. 28, 1997 (Abstract). |
English transation of JP 07330312 (cited by applicants on IDS). * |
Office Action issued Dec. 15, 2010, in Japan Patent Application No. 2005-514938 (with partial English translation). |
Office Action issued May 13, 2011 in Taiwan Patent Application No. 093132259. |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9017582B2 (en) | 2011-05-27 | 2015-04-28 | Chemetall Gmbh | Process for preparing lithium sulfide |
US10865108B2 (en) | 2016-12-14 | 2020-12-15 | Idemitsu Kosan Co., Ltd | Complex comprising sulfur, a method for manufacturing the same, and a method for manufacturing a solid electrolyte |
Also Published As
Publication number | Publication date |
---|---|
KR101109821B1 (ko) | 2012-03-13 |
JP4896520B2 (ja) | 2012-03-14 |
CN1871177B (zh) | 2010-12-22 |
EP1681263A4 (de) | 2008-06-25 |
US20070196739A1 (en) | 2007-08-23 |
TWI366554B (de) | 2012-06-21 |
EP1681263A8 (de) | 2006-10-11 |
EP1681263A1 (de) | 2006-07-19 |
KR20060076316A (ko) | 2006-07-04 |
EP1681263B1 (de) | 2011-06-22 |
CN1871177A (zh) | 2006-11-29 |
CN101980398A (zh) | 2011-02-23 |
WO2005040039A1 (ja) | 2005-05-06 |
JPWO2005040039A1 (ja) | 2007-03-01 |
TW200530121A (en) | 2005-09-16 |
ATE513788T1 (de) | 2011-07-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US8084160B2 (en) | Method for purifying lithium sulfide | |
US8053116B2 (en) | Lithium ion-conductive solid electrolyte | |
JP4873479B2 (ja) | 高性能全固体リチウム電池 | |
JP5690365B2 (ja) | 硫化リチウム粉体の製造方法 | |
US6387340B1 (en) | Manufacturing method for lithium hexafluoro phosphate | |
US20070160911A1 (en) | Lithium ion conducting sulfide based crystallized glass and method for production thereof | |
CN1209393C (zh) | 聚亚芳基硫醚副产物盐的处理方法 | |
US5262137A (en) | Method for recovering lithium chloride | |
JP2000247609A (ja) | 無水アルカリ金属硫化物の製造方法 | |
JP3872846B2 (ja) | 硫化リチウムの製造方法及びポリアリーレンスルフィドの製造方法 | |
JPH0254370B2 (de) | ||
JP3177755B2 (ja) | N−メチルアミノ酪酸リチウムの製造方法 | |
JP3490137B2 (ja) | ポリアリーレンスルフィドの製造方法 | |
CN108178139A (zh) | 一种在制备二氟磷酸锂过程中提高产品收率的方法 | |
JP3446969B2 (ja) | N−メチルアミノ酪酸リチウムの製造方法 | |
JP2000319009A (ja) | 非水酸化リチウム固体状物の分離法 | |
EP4332054A1 (de) | Zusammensetzung mit einem alkalimetallsalz aus bis(fluorsulfonyl)imid | |
EP4332056A1 (de) | Zusammensetzung mit einem alkalimetallsalz aus bis(fluorsulfonyl)imid | |
EP4332055A1 (de) | Zusammensetzung mit einem alkalimetallsalz aus bis(fluorsulfonyl)imid | |
KR20070017190A (ko) | 고성능 전고체 리튬 전지 | |
KR20240086418A (ko) | 불화수소가 저감된 리튬 비스(플루오로설포닐)이미드의 카보네이트 용액 제조방법 | |
KR20230112800A (ko) | 불화수소 함량이 저감된 카보네이트 용제 중의 비스(플루오로설포닐)이미드 리튬염의 제조방법 | |
KR20200114965A (ko) | 불소 음이온의 함유량이 저감된 비스(플루오로설포닐)이미드 리튬염(LiFSI)의 제조 방법 | |
JPH0855620A (ja) | 有機電解質電池用電極及び該電極を用いた有機電解質電池 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: IDEMITSU KOSAN CO., LTD., JAPAN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SEINO, YOSHIKATSU;SENGA, MINORU;REEL/FRAME:027287/0548 Effective date: 20060418 |
|
STCF | Information on status: patent grant |
Free format text: PATENTED CASE |
|
FEPP | Fee payment procedure |
Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
FPAY | Fee payment |
Year of fee payment: 4 |
|
FEPP | Fee payment procedure |
Free format text: MAINTENANCE FEE REMINDER MAILED (ORIGINAL EVENT CODE: REM.); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
LAPS | Lapse for failure to pay maintenance fees |
Free format text: PATENT EXPIRED FOR FAILURE TO PAY MAINTENANCE FEES (ORIGINAL EVENT CODE: EXP.); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |
|
FP | Lapsed due to failure to pay maintenance fee |
Effective date: 20191227 |